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Booster pump sizing calculator

Enter the flow or the number of fixtures, the pressure needed at the critical outlet and the heights. The page computes booster head, parallel pumps with standby, motor size, drive savings and tank volume.

Pre-sizing and estimating tool: results do not replace design, calculations or reports signed by a licensed professional, nor verification against the applicable codes and standards.

Pre-sizing
Design flow
Pressures and heights
Pumps
Drive, energy and tank
—Booster: design flow and head
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Pump curves and required pressure

Parallel pumps at fixed speed versus the constant pressure held by the drive.

Tap the chart to see the values.

Electric power versus demand

Fixed speed (pumps staged in cascade) and drive holding design pressure.

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Next step

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The calculation report gathers this page's inputs, results, equations, assumptions and references, with fields for project, engineer and revision. The full report also includes the charts and interpretations, in color. In the print dialog, choose Save as PDF.

Method, assumptions and references

Equations used

Flow from fixtures: Q = K · n · q, with K = 1 ÷ √(n − 1)
Head: H = (Ppoint − Psuction) ÷ (ρ g) + z + losses; discharge pressure: Pdis = Ppoint + ρ g (z + losses)
Typical single-pump curve (x = q ÷ qdesign): H(x) = H · [h0 − (h0 − 1) x²]; η(x) = ηdesign · (2x − x²); affinity: H ∝ n², q ∝ n
Power: P = ρ g q H ÷ η; motor ≥ power at 120% of design flow (≈ 1.11 × design); drive efficiency 97%
On/off tank: drawdown = qpump · (3600 ÷ z) ÷ 4; Vt = drawdown ÷ [Ppre · (1 ÷ Pon − 1 ÷ Poff)], absolute pressures

Assumptions and limits

  • Identical pumps in parallel; at fixed speed they stage in cascade and share flow equally. With a drive, discharge pressure is held constant at the design value.
  • Energy is estimated at the average demand with a typical radial centrifugal pump curve; the maker’s real curve and an hourly demand profile give a more accurate result.
  • Water at about 68 °F. Friction losses are entered by the user at design flow; the tank is sized for on/off control, and with a drive a smaller tank is usually enough.

Standards and technical documents

  • Hydraulic Institute, ANSI/HI 9.6.3: Rotodynamic Pumps — Guideline for Allowable Operating Region
  • Hydraulic Institute & Europump, Variable Speed Pumping: A Guide to Successful Applications
  • Macintyre, A. J. Instalações Hidráulicas Prediais e Industriais, LTC
  • ASPE Data Book, Volume 2: Plumbing Systems (domestic water booster systems)
  • Karassik, I. J. et al. Pump Handbook, McGraw-Hill

U.S. regulations

  • International Plumbing Code (IPC), Section 604: water supply design, minimum pressures and the 80 psi maximum static pressure (604.8)
  • Uniform Plumbing Code (UPC), Chapter 6: water distribution and booster systems
  • DOE 10 CFR Part 431: efficiency standards for electric motors and clean water pumps

Frequently asked questions

What is a booster pump system?

A set of pumps that raises water pressure when the city main or tank cannot provide enough pressure at the highest or farthest outlets. In buildings, plants and campuses it replaces or supplements a gravity tank. It usually has two or more pumps in parallel with standby, pressure-switch or VFD control and a small tank.

How do I estimate design flow?

Measured peak-hour flow is best. In the US, plumbing codes size domestic water by Hunter’s fixture-unit method (IPC/UPC tables); enter that flow directly. The simple simultaneity option here uses K = 1/√(n − 1): 200 fixtures of 3 gpm at about 7% give 42.5 gpm. For plants, add up equipment that runs at the same time.

How is booster head calculated?

Add the pressure needed at the critical outlet, the elevation to it and the friction losses, then subtract the pressure already available at the suction. In the example: 25 psig at the outlet, 60 ft of elevation and 15 ft of losses, minus 3 psig of suction, give 126 ft and 57.5 psig at the discharge. Losses can come from the valve and fitting pressure drop calculator.

How many pumps should I use?

The most common arrangement is n + 1: duty pumps cover design flow and one stands by, with automatic alternation. Splitting flow between two or three duty pumps improves efficiency at low demand and allows maintenance without cutting water. In the example, 2 + 1 pumps of 21 gpm with 1.5 hp motors.

Is a variable frequency drive worth it?

In most cases, yes: the drive holds constant pressure, avoids overpressure at low demand and cuts starts. In the example, at fixed speed pressure climbs to 71 psig when demand drops, still under the 80 psi IPC limit, and the drive saves 14% of energy, about $145 a year. Savings grow the more time demand stays low.

What tank does a booster need?

With on/off control, the tank limits starts per hour: in the example, 64 gal for up to 30 starts per hour with a 15 psi switch band. With a drive, the tank only holds pressure during zero-demand periods and is usually much smaller; follow the package manufacturer. The hydropneumatic tank calculator details that volume.

What are the most common mistakes?

Overestimating design flow, which leaves big pumps running far from their best point; forgetting maximum pressure at the lowest outlets; and not protecting pumps against dry running. This calculator uses a typical centrifugal pump curve: confirm the selection on the manufacturer’s real curve and check NPSH.